US2754195A - Process for making copper-iron powder - Google Patents

Process for making copper-iron powder Download PDF

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US2754195A
US2754195A US507159A US50715955A US2754195A US 2754195 A US2754195 A US 2754195A US 507159 A US507159 A US 507159A US 50715955 A US50715955 A US 50715955A US 2754195 A US2754195 A US 2754195A
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iron
copper
powder
chloride
hydrogen
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US507159A
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Graham Marion Ernest
William A Reed
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Republic Steel Corp
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Republic Steel Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/16Making metallic powder or suspensions thereof using chemical processes
    • B22F9/18Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
    • B22F9/20Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from solid metal compounds
    • B22F9/22Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from solid metal compounds using gaseous reductors

Definitions

  • This invention relates to a process for making articles consisting essentially of copper and iron, having a high tensile strength and high density and more particularly to a process for making copper-iron powder from which such articles may be fabricated by powder metallurgy methods.
  • This case is related to a copending application of Marion Ernest Graham and William A. Reed entitled Process for Making Copper-Iron Powder, Serial No. 401,064, filed December 29, 1953.
  • This copending application discloses a method for making copper-iron powder by the reduction of iron oxide in the presence of certain reducible copper compounds or metallic copper and particularly in the presence of gaseous hydrogen chloride which must be supplied from an external source.
  • the line of division between the invention of that application and the present invention resides in the fact that the present invention relates to the reduction of certain iron and/r copper compounds by hydrogen.
  • the supplying of gaseous hydrogen chloride from a separate source during reduction is not a necessary feature of the present invention.
  • Said copending application relates to the production of copper-iron powder by a reduction step effective on iron oxide plus a source of copper by hydrogen wherein HCl gas must be supplied from an external source during the reduction.
  • the present case is also a division of our prior and copending application Serial No. 401,063, filed December 29, 1953, for Process for Making Copper-Iron Powder.
  • the line of division between the present case and its parent application Serial No. 401,063 is that the present case is limited to the treatment of a starting mixture including metallic copper with one or more of the chlorides of iron; whereas the parent application, Serial No. 401,- 063, is limited to the treatment of a starting material including metallic iron powder of either of two particular kinds in admixture with an oxide and/or a chloride of copper.
  • High strength and high density articles consisting essentially of copper and iron have found numerous industrial applications, notably in the manufacture of turbine blades and other parts subjected to wear and requiring quite high strength.
  • such parts have been produced by such methods as infiltration of molten copper into iron parts previously prepared by powder metallurgy methods and the coining of parts made from mixtures of copper and iron powders. While such methods may be eifective in producing articles having a high tensile strength, they are objectionable in that they involve substantially more complexity and expense of operation than do powder metallurgy processes.
  • the process of the present invention may be carried out by reducing iron chloride with metallic copper in finely divided form as copper powder, these materials being in intimate admixture prior to the process thereof in accordance with the present invention.
  • the reduction is effected with hydrogen or a gas containing hydrogen. It has been found that in order to produce a copperiron product having the desired physical properties in accordance with the present invention, an actual chemical reduction of the iron chloride must take place while it is in intimate contact with the copper powder as aforesaid. In some cases it may be desirable to produce a metal powder having some predetermined carbon content. To this end it may be necsssary to add a small amount of carbon (e. g. about 1%) to the starting mixture.
  • the starting material is introduced into a reaction zone and there contacted with a reducing gas containing hydrogen.
  • the solid starting material and the reducing gas are both maintained at an elevated temperature in the range of about 1000 F. to about 1800 F. and contact between them is continued until the reduction of the hydrogen-reducible iron compound has been substantially completed.
  • the resultant material is then cooled and, in the event that it be in a massive or semi-sintered condition, is comminuted to powder.
  • This copper-iron powder may then be pressed to a self-sustaining mass of predetermined size and shape, which is subsequently sintered in a suitable non-oxidizing atmosphere usually at a temperature of about 2000 F.
  • a suitable non-oxidizing atmosphere usually at a temperature of about 2000 F.
  • the physical properties of the resulting article will be in part dependent upon the ratio of iron to copper contained therein, the pressure at which it was molded, the sintering temperature and other factors, but in all cases the product of the present invention will have a higher tensile strength than conventional copper-iron parts of the same chemical composition which have been pressed and sintered under similar conditions respectively. In some instances, the tensile strength of articles made in accordance with the process of the present invention will exceed 100,000 pounds per square inch.
  • copper-iron powder suitable for use in powder metallurgy for forming articles having high tensile strength and high density is produced by introducing into a reaction zone a starting material, the essential active ingredients of which consist of: metallic copper powder and a chloride of iron which may be either ferric or ferrous chloride or a mixture of the two and which is hydrogen-reducible; and then contacting said starting material with a reducing gas containing hydrogen as an essential active reducing ingredient under such conditions of temperature and for such a time as to reduce the hydrogen-reducible compound to metallic iron.
  • the ingredients of the starting material are preferably provided in finely-divided form. This further facilitates thorough mixing of the ingredients of the starting material, which is necessary to insure the production of a chemically uniform and homogeneous material.
  • the ingredients used for the starting material must include at least one copper-containing ingredient and at leastiione iron-containingingredient.
  • the copper-containing ingredient in accordance with thepresent invention is metallic copper, which is in finely divided or powder form.
  • the metallic copper used shall have a particle size sufficientlysmall to insure the: product-ion of a'substantially homogeneous. mixture as thestarting material.
  • the sameiconsid'eration is-controlling with: regard to' the particle size oftheironchlori'de ingredient of the starting: material.
  • the iron-containing ingredientof the starting material may be either ferric or ferrous'chloride or armixture of the two. It isbelieved that whenferric chloride, for .example, is. reacted with a suitable reducing agent, such as hydrogen, it is initially converted :to ferrous chloride. as an intermediate stage in the reduction of the iron to its metallic-form or toan oxidation state ofzero. Whether thistheory be accurate or not, ithas been found thatboth the ferric and ferrous forms of iron chloride are equally efiective and as such are the equivalentsof one another for the purposes of the present invention. They areboth intended to be included in the term iron chloride as thatterm is used throughout the presentcase.
  • the'term iron chloride is-meant to include those compounds which decompose easilyunder' the influence of heatto form suchchloride including, for example, the hydrated forms of iron chloride which are known. Because of the low evaporization point of ferric chloride (700 F.), it is somewhat inconvenient. to reduce this compound while mixed with copper since the ferric chloride may vaporize and pass outof contact with the copper before reduction takes place. For this reason it is usually preferred to use ferrous. chloride where iron chloride is required. However, both the ferric and ferrous chlorides are considered equivalents of each other for the purposes of the present invention.
  • the starting material After the ingredients of .the starting material have been selected in accordance with the principles outlined above, they are proportioned so as to result in a reduced powder having the desired ratio of copper-to ironand are thoroughly mixed. In order that thorough mixing :take place, it. is desirable that the starting ingredients be supplied in the-form of powder, and preferably, as finely. divided as is, convenient. In practice it has been found that excellent mixing is obtained by the use of -l: mesh starting materials.
  • Thexrnixeddngredients .maythen be placed in a suitable container, such as a metal boat or pan, and introduced a'nto' a reaction a zone, wherein the hydrogen-reducible iron compound constituent of the starting material is reduced.
  • a suitable container such as a metal boat or pan
  • the chemical reaction be carried to substantial completion.
  • the iron of the hydrogen-reducible iron compound be reduced to. an-oxidation state of zero.
  • This phrase, as used in this description andrthe, appended claims is meant to embrace both the'production of either a physical mixture of elemental metallic powders or the production of some alloy of copper and iron alone or which may be mixed with a simple mixture .of copper and iron.
  • the metallic constituents are presentin an oxidationstate of zero as opposed to the positive oxidation state in which the iron chloride ingredient was introduced in the starting material.
  • Example I Anhydrous "ferrous chloride and metallic copper in flake for-m were blended in a dry state in such proportions-that a completely reduced product would contain about %i-ron and 15% copper-by weight.
  • Themixture was spread on-a tray to a depth of about A inch and the tray placed in an electrically heated mufiie furnace. Dry hydrogen was passed through the furnace over the surface of the mixture at the rate of 6000 cubic centimeters per minute.
  • the temperature of the contents'of the furnace was raised to 1200 F. over a period of about one hour. These conditions of hydrogen-'flow'and temperature were maintained for three additional hours.
  • the sealed inner tube of the furnace was then removedfrom the heating rn'ufl'le and the contents allowed to cool to a temperature below 200 F.
  • the powder was foundby analysis to contain 16.3% metallic copper and 83.7%metallic: iron.
  • This powder was mixed with 1% zinc stearate as -a lubricant, pressed at 50,000 p. s. i. to form'a standard .test bar, which was sintered in hydrogen at 2000'F. for one hour.
  • The'resulting piece had a tensilestrength of 77,500 p. s. i.
  • test bar prepared under identical conditions of pressing andsintering from a-mixture .of' flakev copper and commercial iron powder (madebyithe' reduction of iron oxide) in the proportion 85% ironand 15% copper and tested under parallel conditions had a tensile strengthof only34,300 p. s. i.
  • the process of making copper-iron powder suitable for use in powder metallurgy for forming articles having high tensile strength and high density comprising the steps of introducing into a reaction zone a starting material, the ingredients of which consist essentially of iron in the form of at least one of the chlorides of iron and finely divided metallic copper, and contacting said starting material in said reaction zone and at an elevated temperature with a reducing gas containing hydrogen as its essential active reducing ingredient for a time and under conditions suflicient to reduce the iron of said iron chloride to an oxidation state of zero.

Description

Pnocnss FOR MAKING corPnn-moN POWDER Marion Ernest Graham, Fauna, and William A. Reed,
West Richfield, @hio, assignors to Republic Steel Corporation, Cleveland, Ghio, a corporation of New .lersey No Drawing. Original application December 29, 1953, Serial No. 401,063. Divided and this application May 9, 1955, Serial No. 507,159
3 Claims. (Cl. 75.5) V
This invention relates to a process for making articles consisting essentially of copper and iron, having a high tensile strength and high density and more particularly to a process for making copper-iron powder from which such articles may be fabricated by powder metallurgy methods.
This case is related to a copending application of Marion Ernest Graham and William A. Reed entitled Process for Making Copper-Iron Powder, Serial No. 401,064, filed December 29, 1953. This copending application discloses a method for making copper-iron powder by the reduction of iron oxide in the presence of certain reducible copper compounds or metallic copper and particularly in the presence of gaseous hydrogen chloride which must be supplied from an external source. The line of division between the invention of that application and the present invention resides in the fact that the present invention relates to the reduction of certain iron and/r copper compounds by hydrogen. The supplying of gaseous hydrogen chloride from a separate source during reduction is not a necessary feature of the present invention. Said copending application relates to the production of copper-iron powder by a reduction step effective on iron oxide plus a source of copper by hydrogen wherein HCl gas must be supplied from an external source during the reduction.
The present case is also a division of our prior and copending application Serial No. 401,063, filed December 29, 1953, for Process for Making Copper-Iron Powder. The line of division between the present case and its parent application Serial No. 401,063 is that the present case is limited to the treatment of a starting mixture including metallic copper with one or more of the chlorides of iron; whereas the parent application, Serial No. 401,- 063, is limited to the treatment of a starting material including metallic iron powder of either of two particular kinds in admixture with an oxide and/or a chloride of copper.
High strength and high density articles consisting essentially of copper and iron have found numerous industrial applications, notably in the manufacture of turbine blades and other parts subjected to wear and requiring quite high strength. In the past, such parts have been produced by such methods as infiltration of molten copper into iron parts previously prepared by powder metallurgy methods and the coining of parts made from mixtures of copper and iron powders. While such methods may be eifective in producing articles having a high tensile strength, they are objectionable in that they involve substantially more complexity and expense of operation than do powder metallurgy processes.
It is an object of this invention, therefore, to provide a process'for making articles of high tensile strength consisting essentially of copper and iron that utilizes the relatively simple methods of powder metallurgy.
It is a further object of the invention to provide a process for making copper-iron powder, which is capable of being formed into articles having a high tensile 2,754,195 Patented July 10, 1956 strength and high density by pressing and sintering and without the necessity of infiltration, coining or similar operations.
Other objects of the invention will be in part apparent and in part pointed out by the subsequent description.
The process of the present invention may be carried out by reducing iron chloride with metallic copper in finely divided form as copper powder, these materials being in intimate admixture prior to the process thereof in accordance with the present invention. The reduction is effected with hydrogen or a gas containing hydrogen. It has been found that in order to produce a copperiron product having the desired physical properties in accordance with the present invention, an actual chemical reduction of the iron chloride must take place while it is in intimate contact with the copper powder as aforesaid. In some cases it may be desirable to produce a metal powder having some predetermined carbon content. To this end it may be necsssary to add a small amount of carbon (e. g. about 1%) to the starting mixture.
After the ingredients of the starting material, selected in accordance with the principle outlined above, have been mixed together in the proportions that will result in the desired ratio of iron to copper in the reduced prodnot, the starting material is introduced into a reaction zone and there contacted with a reducing gas containing hydrogen. The solid starting material and the reducing gas are both maintained at an elevated temperature in the range of about 1000 F. to about 1800 F. and contact between them is continued until the reduction of the hydrogen-reducible iron compound has been substantially completed. The resultant material is then cooled and, in the event that it be in a massive or semi-sintered condition, is comminuted to powder. This copper-iron powder may then be pressed to a self-sustaining mass of predetermined size and shape, which is subsequently sintered in a suitable non-oxidizing atmosphere usually at a temperature of about 2000 F. The physical properties of the resulting article will be in part dependent upon the ratio of iron to copper contained therein, the pressure at which it was molded, the sintering temperature and other factors, but in all cases the product of the present invention will have a higher tensile strength than conventional copper-iron parts of the same chemical composition which have been pressed and sintered under similar conditions respectively. In some instances, the tensile strength of articles made in accordance with the process of the present invention will exceed 100,000 pounds per square inch.
Summarizing the present invention, copper-iron powder suitable for use in powder metallurgy for forming articles having high tensile strength and high density is produced by introducing into a reaction zone a starting material, the essential active ingredients of which consist of: metallic copper powder and a chloride of iron which may be either ferric or ferrous chloride or a mixture of the two and which is hydrogen-reducible; and then contacting said starting material with a reducing gas containing hydrogen as an essential active reducing ingredient under such conditions of temperature and for such a time as to reduce the hydrogen-reducible compound to metallic iron.
Since it is an object of the present invention to produce a copper-iron powder, the ingredients of the starting material are preferably provided in finely-divided form. This further facilitates thorough mixing of the ingredients of the starting material, which is necessary to insure the production of a chemically uniform and homogeneous material.
The ingredients used for the starting material must include at least one copper-containing ingredient and at leastiione iron-containingingredient. The copper-containing ingredient in accordance with thepresent invention is metallic copper, which is in finely divided or powder form. This metallic copper may be derived from any: source whatsoever, provided it ispresent' in aform sufii'ciently finely dividedso' that it may be thoroughlymixed with the iron-containing ingredient. In-=practice, it has: been found that copper powder havin'g an average particle-size of about ten microns issatisfactor-ypbut the copper-need not be this-finely dividedto bekus'eful in the process. All thatis required isthat the metallic copper used: shall have a particle size sufficientlysmall to insure the: product-ion of a'substantially homogeneous. mixture as thestarting material. The sameiconsid'eration is-controlling with: regard to' the particle size oftheironchlori'de ingredient of the starting: material.
The iron-containing ingredientof the starting material may be either ferric or ferrous'chloride or armixture of the two. It isbelieved that whenferric chloride, for .example, is. reacted with a suitable reducing agent, such as hydrogen, it is initially converted :to ferrous chloride. as an intermediate stage in the reduction of the iron to its metallic-form or toan oxidation state ofzero. Whether thistheory be accurate or not, ithas been found thatboth the ferric and ferrous forms of iron chloride are equally efiective and as such are the equivalentsof one another for the purposes of the present invention. They areboth intended to be included in the term iron chloride as thatterm is used throughout the presentcase.
-It.is further understood that the'term iron chloride is-meant to include those compounds which decompose easilyunder' the influence of heatto form suchchloride including, for example, the hydrated forms of iron chloride which are known. Because of the low evaporization point of ferric chloride (700 F.), it is somewhat inconvenient. to reduce this compound while mixed with copper since the ferric chloride may vaporize and pass outof contact with the copper before reduction takes place. For this reason it is usually preferred to use ferrous. chloride where iron chloride is required. However, both the ferric and ferrous chlorides are considered equivalents of each other for the purposes of the present invention.
'It is essential to the production of. high strength articles, which is an object of this invention, that the ingredients of the starting material be selected in such a way that at least one of them (a hydrogen-reducibleironchloride) is reduced in the presence of the other (metallic copper). Thus, metallic copper and metallic iron (even iron made in. thepresence of HCl or by reducing iron chloride) and when no hydrogen-reducible material is present, the whole then treated in: hydrogen, did not produce the desired material. Subsequent examples will illustrate that copperironpowder made in this way is definitely inferior as to its tensile strength to copper-iron powder made in accordance withthe teachings of the invention. The fact that a chemical: reduction reaction takes place while the ingredientsare mixed together appears to be necessaryzfor theproduction of the novel copper-iron powder of the present invention, which is capable of producing sintered bodies of unusually high tensile. strength. The reason for thisnovel requirement of the present invention is not fully understood.
'After the ingredients of .the starting material have been selected in accordance with the principles outlined above, they are proportioned so as to result in a reduced powder having the desired ratio of copper-to ironand are thoroughly mixed. In order that thorough mixing :take place, it. is desirable that the starting ingredients be supplied in the-form of powder, and preferably, as finely. divided as is, convenient. In practice it has been found that excellent mixing is obtained by the use of -l: mesh starting materials.
Thexrnixeddngredients .maythen be placed in a suitable container, such as a metal boat or pan, and introduced a'nto' a reaction a zone, wherein the hydrogen-reducible iron compound constituent of the starting material is reduced. In order to insure maximum yield based on the amount of raw material used, it is necessary that the chemical reaction be carried to substantial completion. By this it is meant that the iron of the hydrogen-reducible iron compound be reduced to. an-oxidation state of zero. This phrase, as used in this description andrthe, appended claims, is meant to embrace both the'production of either a physical mixture of elemental metallic powders or the production of some alloy of copper and iron alone or which may be mixed with a simple mixture .of copper and iron. In any case the metallic constituents are presentin an oxidationstate of zero as opposed to the positive oxidation state in which the iron chloride ingredient was introduced in the starting material.
The conditions of reduction are not critical to the success of the process, exceptthat they must be suificient as to both time and temperature as to insure substantially complete reaction between the hydrogenrreducible iron chloride and .the hydrogen-containing gas. In-practice it hasheen found thattemperatures of. the order of 1200 F. are adequate for completing this reduction in about two hours, Lower temperatures, for example. about 1000 F. are fully operative, but require a longer time. Unduly hightemperatures maycause the production of a hard sintered product, which willbe difiicult to grind. This condition is to-heravoided, since one of the objects of the 1 present invention .is the production of pulverulent materiahwhich maybe used in powder metallurgy processes. It has been. found thattemperatures up to 'about 1800 P. will. result in the production of material which is quite frangible and. thus may be comminuted to. powder without undue trouble or expense.
Afterxthe reduction. has been completed, the reduced powder'is cooled in-anon-oxidizing atmosphere toabout 200 F. orv less. The resultantsmass is then'comminuted to; powder, which is then used invarious powder metal.- lurgy processes,- according to standardpractice.
Thesprocess of the present inventionis further illustratedby thefollowing examples,.which are not intended as narrowly limiting upon; the scopeof the present invention.
Example I Anhydrous "ferrous chloride and metallic copper in flake for-m were blended in a dry state in such proportions-that a completely reduced product would contain about %i-ron and 15% copper-by weight. Themixturewas spread on-a tray to a depth of about A inch and the tray placed in an electrically heated mufiie furnace. Dry hydrogen was passed through the furnace over the surface of the mixture at the rate of 6000 cubic centimeters per minute. The temperature of the contents'of the furnacewas raised to 1200 F. over a period of about one hour. These conditions of hydrogen-'flow'and temperature were maintained for three additional hours. The sealed inner tube of the furnace was then removedfrom the heating rn'ufl'le and the contents allowed to cool to a temperature below 200 F. The completely reduced copper-iron product, which had formed into 'a semisintered but easily frangible, cake was then ground to a particle size of about 10() mesh. The powder was foundby analysis to contain 16.3% metallic copper and 83.7%metallic: iron. This powder was mixed with 1% zinc stearate as -a lubricant, pressed at 50,000 p. s. i. to form'a standard .test bar, which was sintered in hydrogen at 2000'F. for one hour. The'resulting piece had a tensilestrength of 77,500 p. s. i. A test bar prepared under identical conditions of pressing andsintering from a-mixture .of' flakev copper and commercial iron powder (madebyithe' reduction of iron oxide) in the proportion 85% ironand 15% copper and tested under parallel conditions had a tensile strengthof only34,300 p. s. i. A
subsequent coiningor similar reworking operation would benecessary'to raise'the strength of this 'latter'pieceto an acceptable value, such reworking being avoided in accordance with the present invention.
As compared with the above, when a reduced metallic iron made by the hydrogen reduction of ferrous chloride is mixed with metallic copper, both metals when mixed being in finely divided form, and mixed in the proportions of 15% copper and 85% iron, then pressed and sintered according to the standard procedure above set forth, a piece having a tensile strength of only 48,200 p. s. i. was obtained. This clearly indicates that an actual chemical reduction must take place while the ingredients of the starting material are in contact with one another in order that the novel and desirable results of the present invention shall be attained.
While there have been disclosed herein several specific processes and certain variants thereof, other alternatives and equivalents will occur to those skilled in the art from the foregoing disclosure. We do not wish to be limited, therefore, except by the scope of the appended claim, which is to be construed validly, as broadly as the state of the prior art permits.
What is claimed is:
l. The process of making copper-iron powder suitable for use in powder metallurgy for forming articles having high tensile strength and high density, comprising the steps of introducing into a reaction zone a starting material, the ingredients of which consist essentially of iron in the form of at least one of the chlorides of iron and finely divided metallic copper, and contacting said starting material in said reaction zone and at an elevated temperature with a reducing gas containing hydrogen as its essential active reducing ingredient for a time and under conditions suflicient to reduce the iron of said iron chloride to an oxidation state of zero.
2. The process according to claim 1, in which the chloride of iron present is reduced in the range of about 1000 F. to about 1200 F.
3. The process according to claim 1, in which the chloride of iron initially present is ferrous chloride, and in which said elevated temperature at which the ferrous chloride is reduced is about 1200 F.
No references cited.

Claims (1)

1. THE PROCESS OF MAKING COPPER-IRON POWDER SUITABLE FOR USE IN POWDER METALLURGY FOR FORMING ARTICLES HAVING HIGH TENSILE STRENGTH AND HIGH DENSITY, COMPRISING THE STEPS OF INTRODUCING INTO A REACTION ZONE A STARTING MATERIAL, THE INGREDIENTS OF WHICH CONSIST ESSENTIALLY OF IRON IN THE FORM OF AT LEAST ONE OF THE CHLORIDES OF IRON AND FINELY DIVIDED METALLIC COPPER, AND CONTACTING SAID STARING MATERIAL IN SAID REACTION ZONE AND AT AN ELEVATED TEMPERATURE WITH A REDUCING GAS CONTAINING HYDROGEN AS ITS ESSENTIAL ACTIVE REDUCING INGREDIENT FOR A TIME AND UNDER CONDITIONS SUFFICIENT TO REDUCE THE IRON OF SAID IRON CHLORIDE TO AN OXIDATION STATE OF ZERO.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3147543A (en) * 1959-04-22 1964-09-08 Du Pont Dispersion hardened metal product
US20090139372A1 (en) * 2003-11-05 2009-06-04 Ishihara Chemical Co, Ltd Production method of pure metal/alloy super-micro powder

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3147543A (en) * 1959-04-22 1964-09-08 Du Pont Dispersion hardened metal product
US20090139372A1 (en) * 2003-11-05 2009-06-04 Ishihara Chemical Co, Ltd Production method of pure metal/alloy super-micro powder
US7799112B2 (en) * 2003-11-05 2010-09-21 Ishihara Chemical Co., Ltd. Production method of pure metal/alloy super-micro powder

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